JP2023183764A - Flocculation evaluation method, flocculation evaluation device, flocculation treatment method, and flocculation treatment system - Google Patents

Flocculation evaluation method, flocculation evaluation device, flocculation treatment method, and flocculation treatment system Download PDF

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JP2023183764A
JP2023183764A JP2022097450A JP2022097450A JP2023183764A JP 2023183764 A JP2023183764 A JP 2023183764A JP 2022097450 A JP2022097450 A JP 2022097450A JP 2022097450 A JP2022097450 A JP 2022097450A JP 2023183764 A JP2023183764 A JP 2023183764A
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water
flocculation
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佳介 瀧口
Keisuke Takiguchi
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Organo Corp
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Japan Organo Co Ltd
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Abstract

To provide a flocculation evaluation method and a flocculation evaluation device that properly evaluate a flocculation state in flocculation treatment.SOLUTION: In a flocculation evaluation method, a flocculation state in flocculation treatment is evaluated, on the basis of water quality information on both water quality of clear water and water quality of concentrated water of a solid-liquid separation apparatus 10 which separates water to be evaluated containing flocculated flocks obtained in the flocculation treatment into clear water and concentrated water.SELECTED DRAWING: Figure 1

Description

本発明は、凝集評価方法、凝集評価装置、凝集処理方法、および凝集処理システムに関する。 The present invention relates to an agglutination evaluation method, an agglutination evaluation device, an agglutination treatment method, and an agglutination treatment system.

水処理において、被処理水中に無機凝集剤や高分子凝集剤等の凝集剤を添加して、懸濁物質等を凝集させてフロックを形成し、凝集フロックを固液分離装置で固液分離する凝集処理が行われる。 In water treatment, a flocculant such as an inorganic flocculant or a polymer flocculant is added to the water to be treated to flocculate suspended solids to form flocs, and the flocs are separated into solid-liquid using a solid-liquid separator. A flocculation process is performed.

このような凝集処理において、被処理水の一部または凝集剤添加後の被処理水の一部を分取し、メインの凝集固液分離装置とは別の固液分離装置に通水して、その処理水の水質を測定することによって判別できる凝集フロックの分離性から凝集の良否を評価したり、その評価結果に基づいてメインの凝集固液分離装置の凝集条件を制御することが知られている(例えば、特許文献1参照)。 In this type of coagulation treatment, a part of the water to be treated or a part of the water to be treated after addition of a coagulant is separated and passed through a solid-liquid separator separate from the main coagulation solid-liquid separator. It is known that the quality of flocculation can be evaluated based on the separability of flocs, which can be determined by measuring the quality of the treated water, and that the flocculation conditions of the main flocculation solid-liquid separation device can be controlled based on the evaluation results. (For example, see Patent Document 1).

低濁度の被処理水を処理する場合、1段の固液分離装置では粒子を十分に分離できず、処理水の水質を測定しても凝集状態を適切に評価できない場合がある。また、固液分離装置における処理水の水質を測定し、凝集フロックの分離性から凝集状態を評価したり制御したりしようとした場合に、分離が不十分であるために、凝集状態の良否によらず処理水質が変わらない場合があり、凝集状態を適切に評価できない。 When treating water with low turbidity, a one-stage solid-liquid separator may not be able to sufficiently separate particles, and the state of aggregation may not be appropriately evaluated even if the quality of the treated water is measured. In addition, when trying to measure the quality of the water treated in the solid-liquid separator and evaluate or control the flocculation state based on the separability of flocs, the separation is insufficient, so it is difficult to determine whether the flocculation state is good or not. In some cases, the quality of the treated water remains the same regardless of the condition, making it impossible to properly evaluate the flocculation state.

特開2019-181342号公報Japanese Patent Application Publication No. 2019-181342

本発明の目的は、凝集処理における凝集状態を適切に評価することができる凝集評価方法、凝集評価装置、およびそれらを用いる凝集処理方法、凝集処理システムを提供することにある。 An object of the present invention is to provide an agglomeration evaluation method, an agglutination evaluation device, and an agglutination treatment method and aggregation treatment system using the same, which can appropriately evaluate the agglomeration state in an aggregation treatment.

本発明は、凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離装置の前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価する、凝集評価方法である。 The present invention provides water quality information on both the quality of the clear water and the quality of the concentrated water of a solid-liquid separator that separates water to be evaluated containing flocculated flocs obtained in a coagulation treatment into clear water and concentrated water. This is an agglomeration evaluation method for evaluating the agglomeration state in the aggregation treatment based on the above-described aggregation treatment.

前記凝集評価方法において、前記水質情報が、前記濃縮水の濁度と前記清澄水の濁度との濁度差であることが好ましい。 In the flocculation evaluation method, it is preferable that the water quality information is a turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water.

前記凝集評価方法において、前記濁度差が小さくなったときに凝集悪化と判断し、前記濁度差が大きくなったときに凝集良好と判断することが好ましい。 In the aggregation evaluation method, it is preferable that when the turbidity difference becomes small, it is determined that the aggregation is deteriorated, and when the turbidity difference becomes large, it is determined that the aggregation is good.

本発明は、凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段と、前記清澄水の水質を測定する清澄水水質測定手段と、前記濃縮水の水質を測定する濃縮水水質測定手段と、を備え、前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価する、凝集評価装置である。 The present invention provides a solid-liquid separation means for separating water to be evaluated containing flocculated flocs obtained by a flocculation treatment into clear water and concentrated water, a clear water quality measuring means for measuring the quality of the clear water, and a clear water quality measuring means for measuring the water quality of the clear water; A flocculation evaluation device, comprising a concentrated water quality measuring means for measuring the water quality of the concentrated water, and evaluating the flocculation state in the flocculation treatment based on water quality information of both the water quality of the clear water and the water quality of the concentrated water. be.

前記凝集評価装置において、前記水質情報が、前記濃縮水の濁度と前記清澄水の濁度との濁度差であることが好ましい。 In the flocculation evaluation device, it is preferable that the water quality information is a turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water.

前記凝集評価装置において、前記濁度差が小さくなったときに凝集悪化と判断し、前記濁度差が大きくなったときに凝集良好と判断することが好ましい。 In the aggregation evaluation device, it is preferable that when the turbidity difference becomes small, it is determined that the aggregation has worsened, and when the turbidity difference becomes large, it is determined that the aggregation is good.

本発明は、被処理水に凝集剤を添加して凝集処理を行う凝集処理工程を含み、前記凝集処理工程で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離装置の前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価する、凝集処理方法である。 The present invention includes a flocculation treatment step in which a flocculant is added to the water to be treated to perform flocculation treatment, and the water to be evaluated containing flocculated flocs obtained in the flocculation treatment step is separated into clear water and concentrated water. The present invention is a flocculation treatment method in which the flocculation state in the flocculation treatment is evaluated based on water quality information of both the water quality of the clear water and the water quality of the concentrated water of the solid-liquid separator.

前記凝集処理方法において、前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理工程における凝集処理の条件を制御することが好ましい。 In the flocculation treatment method, it is preferable to control the conditions of flocculation treatment in the flocculation treatment step based on water quality information of both the water quality of the clear water and the water quality of the concentrated water.

前記凝集処理方法において、前記水質情報が、前記濃縮水の濁度と前記清澄水の濁度との濁度差であることが好ましい。 In the flocculation treatment method, it is preferable that the water quality information is a turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water.

前記凝集処理方法において、前記濁度差が小さくなったときに凝集悪化と判断し、前記濁度差が大きくなったときに凝集良好と判断することが好ましい。 In the aggregation treatment method, it is preferable that when the turbidity difference becomes small, it is determined that the aggregation has worsened, and when the turbidity difference becomes large, it is determined that the aggregation is good.

本発明は、被処理水に凝集剤を添加して凝集処理を行う凝集処理装置と、前記凝集処理装置で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段と、前記清澄水の水質を測定する清澄水水質測定手段と、前記濃縮水の水質を測定する濃縮水水質測定手段と、を備え、前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価する、凝集処理システムである。 The present invention provides a flocculation treatment device that performs flocculation treatment by adding a flocculant to water to be treated, and a flocculation treatment device that separates water to be evaluated containing flocculated flocs obtained by the flocculation treatment device into clear water and concentrated water. A liquid separating means, a clear water quality measuring means for measuring the water quality of the clear water, and a concentrated water water quality measuring means for measuring the water quality of the concentrated water, This is a flocculation treatment system that evaluates the flocculation state in the flocculation treatment based on both types of water quality information.

前記凝集処理システムにおいて、前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理装置における凝集処理の条件を制御する制御手段をさらに備えることが好ましい。 Preferably, the flocculation treatment system further includes a control means for controlling conditions for flocculation treatment in the flocculation treatment device based on water quality information on both the quality of the clear water and the water quality of the concentrated water.

前記凝集処理システムにおいて、前記水質情報が、前記濃縮水の濁度と前記清澄水の濁度との濁度差であることが好ましい。 In the flocculation treatment system, it is preferable that the water quality information is a turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water.

前記凝集処理システムにおいて、前記濁度差が小さくなったときに凝集悪化と判断し、前記濁度差が大きくなったときに凝集良好と判断することが好ましい。 In the aggregation treatment system, it is preferable that when the turbidity difference becomes small, it is determined that the aggregation is deteriorated, and when the turbidity difference becomes large, it is determined that the aggregation is good.

本発明によって、凝集処理における凝集状態を適切に評価することができる凝集評価方法、凝集評価装置、およびそれらを用いる凝集処理方法、凝集処理システムを提供することができる。 According to the present invention, it is possible to provide an agglomeration evaluation method and an agglomeration evaluation apparatus that can appropriately evaluate the agglomeration state in an agglomeration treatment, as well as an aggregation treatment method and an aggregation treatment system using the same.

本発明の実施形態に係る凝集評価装置の一例を示す概略構成図である。1 is a schematic configuration diagram showing an example of an agglomeration evaluation device according to an embodiment of the present invention. 本発明の実施形態に係る凝集評価装置における固液分離装置の一例である曲がりチャネルの流路断面の一例を示す概略図である。It is a schematic diagram showing an example of the flow path cross section of the curved channel which is an example of the solid-liquid separation device in the agglomeration evaluation device according to the embodiment of the present invention. 本発明の実施形態に係る凝集評価装置の他の例を示す概略構成図である。FIG. 3 is a schematic configuration diagram showing another example of the agglomeration evaluation device according to the embodiment of the present invention. 本発明の実施形態に係る凝集評価装置を備える凝集処理システムの一例を示す概略構成図である。1 is a schematic configuration diagram showing an example of an agglomeration processing system including an aggregation evaluation device according to an embodiment of the present invention. 実施例1における濁度の経時変化を示すグラフである。3 is a graph showing changes in turbidity over time in Example 1. 比較例1における濁度の経時変化を示すグラフである。3 is a graph showing changes in turbidity over time in Comparative Example 1.

本発明の実施の形態について以下説明する。本実施形態は本発明を実施する一例であって、本発明は本実施形態に限定されるものではない。 Embodiments of the present invention will be described below. This embodiment is an example of implementing the present invention, and the present invention is not limited to this embodiment.

本発明の実施形態に係る凝集評価装置の一例の概略を図1に示し、その構成について説明する。 An example of an agglomeration evaluation device according to an embodiment of the present invention is schematically shown in FIG. 1, and its configuration will be described.

図1の凝集評価装置1は、凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段として、固液分離装置10と、清澄水の水質を測定する清澄水水質測定手段として、清澄水水質測定装置12と、濃縮水の水質を測定する濃縮水水質測定手段として、濃縮水水質測定装置14と、を備える。 The flocculation evaluation apparatus 1 in FIG. 1 includes a solid-liquid separator 10 as a solid-liquid separation means for separating evaluated water containing flocculated flocs obtained by flocculation treatment into clear water and concentrated water. A clear water quality measuring device 12 is provided as a clear water quality measuring means for measuring the water quality of concentrated water, and a concentrated water quality measuring device 14 is provided as a concentrated water quality measuring means for measuring the water quality of concentrated water.

図1の凝集評価装置1において、固液分離装置10の入口には、被評価水配管16が接続されている。固液分離装置10の清澄水出口には、清澄水配管18が接続され、濃縮水出口には、濃縮水配管20が接続されている。清澄水配管18には、清澄水水質測定装置12が設置され、濃縮水配管20には、濃縮水水質測定装置14が設置されている。 In the flocculation evaluation apparatus 1 shown in FIG. 1, an evaluation target water pipe 16 is connected to the inlet of the solid-liquid separator 10. A clear water pipe 18 is connected to a clear water outlet of the solid-liquid separator 10, and a concentrated water pipe 20 is connected to a concentrated water outlet. A clear water quality measuring device 12 is installed in the clear water pipe 18, and a concentrated water quality measuring device 14 is installed in the concentrated water pipe 20.

本実施形態に係る凝集評価方法および凝集評価装置1の動作について説明する。 The agglomeration evaluation method and the operation of the agglomeration evaluation device 1 according to the present embodiment will be described.

凝集処理で得られた凝集フロックを含む被評価水は、被評価水配管16を通して固液分離装置10に供給され、固液分離装置10において、清澄水と濃縮水とに分離される(固液分離工程)。清澄水は、清澄水配管18を通して排出され、濃縮水は、濃縮水配管20を通して排出される。 The evaluated water containing flocculated flocs obtained in the coagulation process is supplied to the solid-liquid separator 10 through the evaluated water piping 16, and is separated into clear water and concentrated water in the solid-liquid separator 10. separation process). Clear water is discharged through clear water piping 18 and concentrated water is discharged through concentrated water piping 20.

清澄水配管18において、清澄水水質測定装置12によって清澄水の水質が測定され、清澄水の水質情報が取得される(清澄水水質測定工程)。濃縮水配管20において、濃縮水水質測定装置14によって濃縮水の水質が測定され、濃縮水の水質情報が取得される(濃縮水水質測定工程)。 In the clear water pipe 18, the quality of the clear water is measured by the clear water quality measurement device 12, and the water quality information of the clear water is acquired (clear water quality measurement step). In the concentrated water piping 20, the quality of the concentrated water is measured by the concentrated water quality measuring device 14, and water quality information of the concentrated water is acquired (concentrated water quality measuring step).

本実施形態に係る凝集評価方法および凝集評価装置では、固液分離装置10で清澄側と濃縮側とに分離を行い、清澄側と濃縮側の両方の水質情報に基づいて凝集状態を評価する。これによって、凝集処理における凝集状態を適切に評価することができる。また、低濁度(例えば、5度以下)の被評価水であっても、凝集処理における凝集状態を適切に評価することができる。固液分離装置10における分離が不十分であっても、凝集処理における凝集状態を適切に評価することができる。 In the flocculation evaluation method and flocculation evaluation apparatus according to the present embodiment, the solid-liquid separator 10 performs separation into a clarification side and a concentration side, and evaluates the flocculation state based on water quality information on both the clarification side and the concentration side. Thereby, the aggregation state in the aggregation process can be appropriately evaluated. Moreover, even if the water to be evaluated has a low turbidity (for example, 5 degrees or less), the flocculation state in the flocculation treatment can be appropriately evaluated. Even if the separation in the solid-liquid separator 10 is insufficient, the state of aggregation in the aggregation process can be appropriately evaluated.

固液分離装置10は、例えば、曲がり配管を用いた曲がりチャネルによって発達したディーン渦を利用して分離するセルや、重力沈降、膜ろ過、砂ろ過等による固液分離装置が挙げられるが、分離速度やメンテナンス性等の観点から、ディーン渦を利用した曲がりチャネルが好ましい。 The solid-liquid separator 10 includes, for example, a cell that separates using a Dean vortex developed by a curved channel using bent pipes, and a solid-liquid separator that uses gravity sedimentation, membrane filtration, sand filtration, etc. From the viewpoint of speed and maintainability, a curved channel using a Dean vortex is preferable.

曲がりチャネルは、被処理液(被評価水)を流入するための被処理液入口と、流体が流れるための例えば矩形状の1つの流路を有する配管が渦巻き状に形成された渦巻き状チャネルと、清澄水(チャネル処理水)を排出するための、流路の例えば外周側から分かれた清澄水出口と、濃縮水(チャネル濃縮水)を排出するための、流路の例えば内周側から分かれた濃縮水出口と、を有する。図2に曲がりチャネルの流路の断面を示すが、固体粒子(凝集物)を含む被処理液が被処理液入口から渦巻き状チャネルに導入されると、矩形状の流路の断面には二次流れ(ディーン渦)が生じる。これは遠心力による外向きの流れと、直進しようとする流れが外壁により強制的に曲げられることによる内向きへの圧力によるものである。 The curved channel is a spiral channel in which piping is formed in a spiral shape and has a to-be-treated liquid inlet for inflowing the to-be-treated liquid (water to be evaluated) and one rectangular flow path for the fluid to flow. , a clear water outlet separated from, for example, the outer circumferential side of the flow path for discharging clear water (channel treated water), and a clear water outlet separated from, for example, the inner circumference side of the flow path for discharging concentrated water (channel concentrated water). and a concentrated water outlet. Figure 2 shows a cross section of the curved channel. When a liquid to be treated containing solid particles (agglomerates) is introduced into the spiral channel from the inlet of the liquid to be treated, the cross section of the rectangular channel has two parts. A secondary flow (Dean vortex) is generated. This is due to the outward flow due to centrifugal force and the inward pressure caused by the flow that is trying to proceed straight to be forcibly bent by the outer wall.

固体粒子はこの二次流れ(ディーン渦)の中では内周側に集まるとされるが、固体粒子の密度、流路中を流れる流体の流束、流路の曲率等のバランスによっては、固体粒子が外周側に集まる場合もある。この場合には、曲がりチャネルは、流路の内周側から分かれた清澄水出口と、流路の外周側から分かれた濃縮水出口と、を有していてもよい。曲がりチャネルは、曲がりチャネルにおける固体粒子の密度、流路中を流れる流体の流束、流路の曲率等のバランスを調整することにより、固体粒子と液体との密度差と、重力と、流体力学的作用とによって、被処理液から固体粒子を分離することができる。 Solid particles are said to gather on the inner circumferential side of this secondary flow (Dean vortex), but depending on the balance of the density of the solid particles, the flux of the fluid flowing in the flow path, the curvature of the flow path, etc. Particles may also collect on the outer periphery. In this case, the curved channel may have a clear water outlet separated from the inner circumference side of the flow path and a concentrated water outlet separated from the outer circumference side of the flow path. By adjusting the balance of the density of solid particles in the curved channel, the flux of the fluid flowing in the flow path, the curvature of the flow path, etc., the curved channel can reduce the density difference between solid particles and liquid, gravity, and fluid dynamics. Solid particles can be separated from the liquid to be treated by the chemical action.

曲がりチャネルは、曲率を有する壁面を含む流路を有するものであればよく、特に制限はない。曲がりチャネルは、例えば、曲率を有する壁面を含む1つの流路を有する配管が渦巻き状に形成されたものである。曲がりチャネルの流路の断面形状は、矩形状、円状、楕円状等が挙げられ、ディーン渦の形成のためには、流路の断面形状が矩形状であることが望ましい。すなわち、曲がりチャネルは、上壁面と下壁面と曲率を有する側壁面とを含む流路を有する。 The curved channel is not particularly limited as long as it has a flow path including a wall surface with curvature. A curved channel is, for example, a pipe formed in a spiral shape and having one flow path including a wall surface having a curvature. The cross-sectional shape of the flow path of the curved channel may be rectangular, circular, elliptical, etc., and in order to form a Dean vortex, it is desirable that the cross-sectional shape of the flow path is rectangular. That is, the curved channel has a flow path including an upper wall surface, a lower wall surface, and a side wall surface having curvature.

被処理液の流量に応じて曲がりチャネルの内側に固体粒子が濃縮されるのか、外側に濃縮されるのかが変わるため、チャネル処理水配管およびチャネル濃縮水配管は、被処理液の流量に応じて適宜変更してもよい。 Depending on the flow rate of the liquid to be treated, whether the solid particles are concentrated inside or outside the curved channel changes, so the channel treated water piping and channel concentrated water piping are It may be changed as appropriate.

曲がりチャネルは、固体粒子の分離の目的に応じて決められた所定の曲率、長さ、および幅を有することが好ましい。 Preferably, the curved channel has a predetermined curvature, length, and width determined depending on the purpose of separating solid particles.

固体粒子の分離に最適となる曲がりチャネルの仕様は、固体粒子の性状(密度、粒子径等)によって変化するため、流動解析ソフトを用いて決定することが望ましい。流動解析ソフトとしては、例えば、「ANSYS Fluent」(ANSYS社)等が挙げられる。 The specifications of the curved channel that are optimal for separating solid particles vary depending on the properties of the solid particles (density, particle size, etc.), so it is desirable to determine them using flow analysis software. Examples of the flow analysis software include "ANSYS Fluent" (ANSYS, Inc.).

清澄水および濃縮水の水質測定はバルブの切り替え等によって、1つの水質測定装置を使用して濃縮水と清澄水の両方の水質を測定してもよい。 The water quality of clear water and concentrated water may be measured by switching valves or the like, using one water quality measuring device.

測定する水質としては、例えば、濁度、色度、有機物濃度(TOC)、pH、画像および画像解析により得られる数値(例えば、粒子数、粒子径、フロックの色、機械学習やディープラーニングを用いた画像解析およびフロックの状態評価)等が挙げられる。凝集状態を評価する場合には、水質測定装置の価格等を考慮して濁度を測定する濁度計が望ましい。 The water quality to be measured includes, for example, turbidity, chromaticity, organic matter concentration (TOC), pH, images, and numerical values obtained by image analysis (e.g., particle number, particle size, floc color, and measurements using machine learning and deep learning). image analysis and floc condition evaluation). When evaluating the flocculation state, a turbidity meter that measures turbidity is preferable, taking into consideration the price of the water quality measuring device.

水質情報は、例えば、濃縮水の濁度と清澄水の濁度との濁度差、濃縮水の濁度と清澄水の濁度との比率、または濃縮水の濁度と清澄水の濁度の合計値に対する清澄水濁度の比率等が挙げられる。例えば、水質情報として濃縮水の濁度と清澄水の濁度との濁度差を用いる場合、凝集が良好な状態では、固液分離装置10において濃縮水の濁度が上昇し、清澄水との濁度の差が大きくなる。一方で凝集状態が悪い場合には、濃縮水と清澄水の濁度の差が小さくなる。したがって、濃縮水の濁度と清澄水の濁度との濁度差が小さくなったときに凝集悪化と判断し、濁度差が大きくなったときに凝集良好と判断すればよい。 The water quality information is, for example, the turbidity difference between the turbidity of concentrated water and the turbidity of clear water, the ratio between the turbidity of concentrated water and the turbidity of clear water, or the turbidity of concentrated water and the turbidity of clear water. Examples include the ratio of clear water turbidity to the total value of . For example, when using the turbidity difference between the turbidity of concentrated water and the turbidity of clear water as water quality information, when the flocculation is good, the turbidity of the concentrated water increases in the solid-liquid separator 10, and the turbidity of the concentrated water increases. The difference in turbidity increases. On the other hand, if the aggregation state is poor, the difference in turbidity between concentrated water and clear water becomes small. Therefore, when the turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water becomes small, it is determined that the aggregation is deteriorated, and when the turbidity difference becomes large, it is determined that the aggregation is good.

被評価水の水質を測定する被評価水水質測定手段として、被評価水水質測定装置を例えば被評価水配管16に設置し、被評価水の水質を測定して、被評価水の水質、固液分離装置10の清澄水の水質および濃縮水の水質の水質情報に基づいて凝集処理における凝集状態を評価してもよい。これによって、凝集処理における凝集状態をより適切に評価することができる。 As an evaluation water quality measuring means for measuring the water quality of the evaluation water, an evaluation water quality measuring device is installed, for example, in the evaluation water piping 16, and the water quality of the evaluation water is measured. The flocculation state in the flocculation process may be evaluated based on the water quality information of the clear water quality and the concentrated water quality of the liquid separation device 10. Thereby, the agglomeration state in the aggregation process can be evaluated more appropriately.

凝集評価装置は、清澄水水質測定装置12により測定された清澄水の水質および濃縮水水質測定装置14により測定された濃縮水の水質に基づいて所定の出力を行う出力手段として、出力部を備えてもよい。清澄水水質測定装置12および濃縮水水質測定装置14には、出力部が設置されていてもよい。出力部は、清澄水水質測定装置12および濃縮水水質測定装置14のそれぞれに設置されていてもよいし、共通で1つ設置されていてもよい。清澄水水質測定装置12により測定された清澄水の水質および濃縮水水質測定装置14により測定された濃縮水の水質に基づいて、出力部において例えば凝集悪化を知らせる警報等の所定の出力が行われてもよい(出力工程)。 The flocculation evaluation device includes an output section as an output means for outputting a predetermined output based on the quality of clear water measured by the clear water quality measuring device 12 and the quality of concentrated water measured by the concentrated water quality measuring device 14. You can. The clear water quality measuring device 12 and the concentrated water quality measuring device 14 may be provided with an output section. The output unit may be installed in each of the clear water quality measuring device 12 and the concentrated water quality measuring device 14, or one output unit may be installed in common. Based on the water quality of the clear water measured by the clear water quality measuring device 12 and the water quality of the concentrated water measured by the concentrated water water quality measuring device 14, a predetermined output such as an alarm to notify deterioration of aggregation is performed at the output section. (output process).

出力部における出力としては、凝集悪化を知らせる表示や音等の視聴覚的に認知可能な警報の他に、凝集状態の変化に対応するための対応方法等が表示されてもよい。出力部は、例えば、情報を表示、出力することができるものであればよく、特に制限はないが、例えば、液晶ディスプレイ、有機ELディスプレイ等の表示手段や、スピーカ等の音声出力手段等が挙げられる。例えば、警報の方法としては、制御盤のタッチパネル上に表示する、インターネット通信を介して運転員に通知する、監視室等に通知する等が挙げられる。 As the output from the output unit, in addition to an audiovisually perceptible alarm such as a display or sound that indicates deterioration of aggregation, a response method for responding to a change in the aggregation state, etc. may be displayed. The output unit is not particularly limited as long as it can display and output information, but examples include display means such as a liquid crystal display and organic EL display, and audio output means such as a speaker. It will be done. For example, methods of issuing an alarm include displaying it on a touch panel of a control panel, notifying an operator via Internet communication, and notifying a monitoring room or the like.

出力部は、例えば濃縮水の濁度と清澄水の濁度との濁度差が所定の閾値を下回った場合に警報を出してもよい。警報の閾値は、1つに予め決めてもよいし、被処理水の濁度等の水質に応じて段階的、比例的に変化させてもよい。 The output unit may issue an alarm, for example, when the turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water falls below a predetermined threshold. The alarm threshold value may be set in advance to one value, or may be changed stepwise or proportionally depending on the water quality such as turbidity of the water to be treated.

濃縮水と清澄水の濁度差をより明確にするために、固液分離を2段以上にしてもよい。固液分離を2段とした場合の凝集評価装置の一例を図3に示す。 In order to make the difference in turbidity between concentrated water and clear water more clear, solid-liquid separation may be performed in two or more stages. FIG. 3 shows an example of an agglomeration evaluation device in which solid-liquid separation is performed in two stages.

図3の凝集評価装置3は、凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段として、第1固液分離装置30および第2固液分離装置32と、清澄水の水質を測定する清澄水水質測定手段として、清澄水水質測定装置36と、濃縮水の水質を測定する濃縮水水質測定手段として、濃縮水水質測定装置34と、を備える。 The flocculation evaluation apparatus 3 in FIG. 3 includes a first solid-liquid separator 30 and a second solid-liquid separator as a solid-liquid separation means for separating water to be evaluated containing flocculated flocs obtained by flocculation treatment into clear water and concentrated water. A liquid separation device 32, a clear water quality measuring device 36 as a clear water quality measuring means for measuring the water quality of clear water, a concentrated water quality measuring device 34 as a concentrated water quality measuring means for measuring the water quality of concentrated water, Equipped with.

図3の凝集評価装置3において、第1固液分離装置30の入口には、被評価水配管38が接続されている。第1固液分離装置30の第1清澄水出口と第2固液分離装置32の入口とは、第1清澄水配管40により接続され、第1固液分離装置30の第1濃縮水出口には、第1濃縮水配管42が接続されている。第2固液分離装置32の第2清澄水出口には、第2清澄水配管44が接続され、第2濃縮水出口には、第2濃縮水配管46が接続されている。第2清澄水配管44には、清澄水水質測定装置36が設置され、第1濃縮水配管42には、濃縮水水質測定装置34が設置されている。 In the flocculation evaluation device 3 of FIG. 3, an evaluation target water pipe 38 is connected to the inlet of the first solid-liquid separation device 30. The first clear water outlet of the first solid-liquid separator 30 and the inlet of the second solid-liquid separator 32 are connected by a first clear water pipe 40, and are connected to the first concentrated water outlet of the first solid-liquid separator 30. is connected to the first concentrated water pipe 42. A second clear water pipe 44 is connected to the second clear water outlet of the second solid-liquid separator 32, and a second concentrated water pipe 46 is connected to the second concentrated water outlet. A clear water quality measuring device 36 is installed in the second clear water pipe 44, and a concentrated water quality measuring device 34 is installed in the first concentrated water pipe 42.

凝集処理で得られた凝集フロックを含む被評価水は、被評価水配管38を通して第1固液分離装置30に供給され、第1固液分離装置30において、第1清澄水と第1濃縮水とに分離される(第1固液分離工程)。第1濃縮水は、第1濃縮水配管42を通して排出される。 The water to be evaluated containing flocculated flocs obtained by the coagulation process is supplied to the first solid-liquid separator 30 through the water to be evaluated piping 38, and in the first solid-liquid separator 30, the first clear water and the first concentrated water are separated. (first solid-liquid separation step). The first concentrated water is discharged through the first concentrated water pipe 42.

第1固液分離装置30で得られた第1清澄水は、第1清澄水配管40を通して第2固液分離装置32に供給され、第2固液分離装置32において、第2清澄水と第2濃縮水とに分離される(第2固液分離工程)。第2清澄水は、第2清澄水配管44を通して排出され、第2濃縮水は、第2濃縮水配管46を通して排出される。 The first clear water obtained in the first solid-liquid separator 30 is supplied to the second solid-liquid separator 32 through the first clear water pipe 40, and in the second solid-liquid separator 32, the first clear water is mixed with the second clear water. 2 concentrated water (second solid-liquid separation step). The second clear water is discharged through the second clear water pipe 44 , and the second concentrated water is discharged through the second concentrated water pipe 46 .

第2清澄水配管44において、清澄水水質測定装置36によって第2清澄水の水質が測定され、第2清澄水の水質情報が取得される(清澄水水質測定工程)。第1濃縮水配管42において、濃縮水水質測定装置34によって第1濃縮水の水質が測定され、第1濃縮水の水質情報が取得される(濃縮水水質測定工程)。 In the second clear water pipe 44, the quality of the second clear water is measured by the clear water quality measurement device 36, and water quality information of the second clear water is acquired (clear water quality measurement step). In the first concentrated water piping 42, the quality of the first concentrated water is measured by the concentrated water quality measuring device 34, and water quality information of the first concentrated water is acquired (concentrated water quality measuring step).

本実施形態に係る凝集評価方法および凝集評価装置では、第1固液分離装置30で清澄側と濃縮側とに分離を行い、第1固液分離装置30の清澄側について第2固液分離装置32で清澄側と濃縮側とに分離を行い、最終段の清澄側と第1段の濃縮側の両方の水質情報に基づいて凝集状態を評価する。これによって、凝集処理における凝集状態を適切に評価することができる。 In the flocculation evaluation method and flocculation evaluation apparatus according to the present embodiment, the first solid-liquid separator 30 performs separation into the clarifying side and the concentration side, and the clarifying side of the first solid-liquid separator 30 is separated into the second solid-liquid separator 30. At step 32, the water is separated into the clarification side and the concentration side, and the flocculation state is evaluated based on the water quality information from both the final stage clarification side and the first stage concentration side. Thereby, the aggregation state in the aggregation process can be appropriately evaluated.

固液分離を2段以上にすることによって、清澄側と濃縮側との濁度差が明確になり、制御に利用しやすくなる。 By performing solid-liquid separation in two or more stages, the difference in turbidity between the clarification side and the concentration side becomes clear, making it easier to use for control.

固液分離を2段以上とした場合、清澄水の水質測定は、最終段の固液分離装置の清澄水について行えばよく、濃縮水の水質測定は、第1段の固液分離装置の濃縮水について行えばよい。または、各段の濃縮水および最終段の清澄水について水質測定を行い、各段の濃縮側と最終段の清澄側の各水質情報に基づいて凝集状態を評価してもよい。 When solid-liquid separation is performed in two or more stages, the water quality measurement of the clear water can be performed on the clear water in the final stage solid-liquid separator, and the water quality measurement on the concentrated water can be performed on the water quality of the concentrated water in the first stage solid-liquid separator. Just follow the water. Alternatively, the water quality may be measured for the concentrated water in each stage and the clarified water in the final stage, and the flocculation state may be evaluated based on the water quality information on the concentrated water in each stage and the clarified water in the final stage.

濃縮水と清澄水の水質に応じて、メインフローとなる凝集処理装置における凝集処理の条件を制御してもよい。このような場合の凝集処理システムの一例を図4に示す。 Depending on the quality of the concentrated water and the clear water, the conditions of the flocculation process in the flocculation treatment device that is the main flow may be controlled. An example of an aggregation treatment system in such a case is shown in FIG.

図4の凝集処理システム7は、被処理水に凝集剤を添加して凝集処理を行う凝集処理手段として、凝集処理装置5と、凝集処理における凝集状態を評価する凝集評価装置3と、を備える。凝集処理システム7における凝集評価装置3は、清澄水の水質および濃縮水の水質の両方の水質情報に基づいて凝集処理装置5における凝集処理の条件を制御する制御手段として、制御装置70を備えてもよい。 The flocculation treatment system 7 in FIG. 4 includes a flocculation treatment device 5 as a flocculation treatment means for performing flocculation treatment by adding a flocculant to the water to be treated, and a flocculation evaluation device 3 for evaluating the flocculation state in the flocculation treatment. . The flocculation evaluation device 3 in the flocculation treatment system 7 includes a control device 70 as a control means for controlling the conditions of flocculation treatment in the flocculation treatment device 5 based on water quality information of both the water quality of clear water and the water quality of concentrated water. Good too.

凝集評価装置3は、凝集処理装置5における凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段として、第1固液分離装置30および第2固液分離装置32と、清澄水の水質を測定する清澄水水質測定手段として、清澄水水質測定装置36と、濃縮水の水質を測定する濃縮水水質測定手段として、濃縮水水質測定装置34と、を備える。 The flocculation evaluation device 3 serves as a solid-liquid separation means for separating the evaluated water containing flocculated flocs obtained by the flocculation treatment in the flocculation treatment device 5 into clear water and concentrated water. 2 solid-liquid separator 32, a clear water quality measuring device 36 as a clear water quality measuring means for measuring the water quality of clear water, and a concentrated water quality measuring device 34 as a concentrated water quality measuring means for measuring the water quality of concentrated water. and.

凝集処理装置5は、被処理水に凝集剤を添加して混和するための凝集混和手段として、凝集混和槽50と、形成されたフロックを含む凝集濃縮水と処理水とに分離するための分離手段として、分離装置52とを備える。凝集処理装置5は、凝集混和槽50と分離装置52との間に、混和された混和液中にフロックを形成するためのフロック形成手段として、フロック形成槽を設けてもよい。凝集処理装置5は、分離装置52の後段に、処理水についてろ過処理を行うろ過処理手段として、砂ろ過装置を備えてもよい。 The coagulation treatment device 5 includes a coagulation mixing tank 50 as a coagulation mixing means for adding and mixing a coagulant to the water to be treated, and a separation device for separating the coagulation concentrated water containing formed flocs and treated water. As a means, a separation device 52 is provided. The flocculation treatment device 5 may provide a floc formation tank between the flocculation mixing tank 50 and the separation device 52 as a floc formation means for forming flocs in the mixed liquid mixture. The aggregation treatment device 5 may include a sand filter device downstream of the separation device 52 as a filtration treatment means that performs a filtration treatment on the treated water.

凝集処理装置5において、凝集混和槽50の入口には、被処理水配管54が接続されている。凝集混和槽50の出口と分離装置52の入口とは、凝集液配管56により接続されている。分離装置52の出口には、処理水配管58が接続されている。凝集混和槽50の薬剤入口には、凝集剤添加手段として、凝集剤添加配管60が接続されている。 In the coagulation treatment device 5 , a water pipe 54 to be treated is connected to the inlet of the coagulation mixing tank 50 . The outlet of the coagulation mixing tank 50 and the inlet of the separation device 52 are connected by a coagulation liquid piping 56. A treated water pipe 58 is connected to the outlet of the separation device 52. A flocculant addition pipe 60 is connected to the chemical inlet of the flocculation mixing tank 50 as a flocculant addition means.

凝集混和槽50の被評価水出口と第1固液分離装置30の入口とは、被評価水配管38により接続されている。第1固液分離装置30の第1清澄水出口と第2固液分離装置32の入口とは、第1清澄水配管40により接続され、第1固液分離装置30の第1濃縮水出口には、第1濃縮水配管42が接続されている。第2固液分離装置32の第2清澄水出口には、第2清澄水配管44が接続され、第2濃縮水出口には、第2濃縮水配管46が接続されている。第2清澄水配管44には、清澄水水質測定装置36が設置され、第1濃縮水配管42には、濃縮水水質測定装置34が設置されている。 The evaluated water outlet of the flocculation mixing tank 50 and the inlet of the first solid-liquid separator 30 are connected by an evaluated water pipe 38. The first clear water outlet of the first solid-liquid separator 30 and the inlet of the second solid-liquid separator 32 are connected by a first clear water pipe 40, and are connected to the first concentrated water outlet of the first solid-liquid separator 30. is connected to the first concentrated water pipe 42. A second clear water pipe 44 is connected to the second clear water outlet of the second solid-liquid separator 32, and a second concentrated water pipe 46 is connected to the second concentrated water outlet. A clear water quality measuring device 36 is installed in the second clear water pipe 44, and a concentrated water quality measuring device 34 is installed in the first concentrated water pipe 42.

制御装置70は、濃縮水水質測定装置34、清澄水水質測定装置36、凝集剤添加配管60に設置された凝集剤の添加量を調整する凝集剤添加量調整手段(図示せず)、例えば、バルブ、ポンプ等とは、有線または無線の電気的接続等によりそれぞれ接続されている。 The control device 70 includes a flocculant addition amount adjusting means (not shown) installed in the concentrated water quality measurement device 34, the clear water quality measurement device 36, and the flocculant addition piping 60 for adjusting the amount of flocculant added, for example, The valves, pumps, etc. are connected to each other by wired or wireless electrical connections.

例えば、懸濁物質等を含む被処理水は、被処理水配管54を通して凝集混和槽50に送液される。凝集混和槽50において、凝集剤添加配管60を通して被処理水に凝集剤が添加され、急速撹拌されて凝集が行われ(凝集混和工程)、フロックが形成される(フロック形成工程)。凝集混和槽50の後段にフロック形成槽を設けてフロック形成槽においてフロックが形成されてもよい。凝集混和槽50において、被処理水にpH調整剤が添加されて、pH調整が行われてもよい(pH調整工程)。形成されたフロックを含む凝集液は、凝集液配管56を通して分離装置52へと送液されて、分離装置52において重力による沈降分離、ろ過等により固液分離が行われて、処理水が得られる(分離工程)(以上が、凝集処理工程)。処理水は、分離装置52の後段の砂ろ過装置へ送液され、砂ろ過装置においてろ過処理が行われてもよい(ろ過処理工程)。 For example, the water to be treated containing suspended matter and the like is sent to the coagulation mixing tank 50 through the water to be treated piping 54 . In the flocculant-mixing tank 50, a flocculant is added to the water to be treated through the flocculant addition pipe 60, and the water is rapidly stirred to perform flocculation (coagulation-mixing step) to form flocs (floc-forming step). A flocculation tank may be provided after the flocculation mixing tank 50, and flocs may be formed in the flocculation tank. In the coagulation mixing tank 50, a pH adjuster may be added to the water to be treated to adjust the pH (pH adjustment step). The flocculated liquid containing the formed flocs is sent to the separation device 52 through the flocculation liquid piping 56, where solid-liquid separation is performed by gravity sedimentation, filtration, etc., and treated water is obtained. (Separation process) (The above is the aggregation treatment process). The treated water may be sent to a sand filtration device downstream of the separation device 52 and subjected to filtration treatment in the sand filtration device (filtration treatment step).

凝集処理装置5で得られた凝集フロックを含む凝集混和水は、凝集混和槽50から枝分かれして被評価水として被評価水配管38を通して第1固液分離装置30に供給され、第1固液分離装置30において、第1清澄水と第1濃縮水とに分離される(第1固液分離工程)。第1濃縮水は、第1濃縮水配管42を通して排出される。 The flocculated mixed water containing flocculated flocs obtained in the flocculation treatment device 5 is branched from the flocculation mixing tank 50 and is supplied as water to be evaluated to the first solid-liquid separator 30 through the water to be evaluated piping 38. In the separation device 30, the water is separated into first clear water and first concentrated water (first solid-liquid separation step). The first concentrated water is discharged through the first concentrated water pipe 42.

第1固液分離装置30で得られた第1清澄水は、第1清澄水配管40を通して第2固液分離装置32に供給され、第2固液分離装置32において、第2清澄水と第2濃縮水とに分離される(第2固液分離工程)。第2清澄水は、第2清澄水配管44を通して排出され、第2濃縮水は、第2濃縮水配管46を通して排出される。 The first clear water obtained in the first solid-liquid separator 30 is supplied to the second solid-liquid separator 32 through the first clear water pipe 40, and in the second solid-liquid separator 32, the first clear water is mixed with the second clear water. 2 concentrated water (second solid-liquid separation step). The second clear water is discharged through the second clear water pipe 44 , and the second concentrated water is discharged through the second concentrated water pipe 46 .

第2清澄水配管44において、清澄水水質測定装置36によって第2清澄水の水質が測定され、第2清澄水の水質情報が取得される(清澄水水質測定工程)。第1濃縮水配管42において、濃縮水水質測定装置34によって第1濃縮水の水質が測定され、第1濃縮水の水質情報が取得される(濃縮水水質測定工程)。 In the second clear water pipe 44, the quality of the second clear water is measured by the clear water quality measurement device 36, and water quality information of the second clear water is acquired (clear water quality measurement step). In the first concentrated water piping 42, the quality of the first concentrated water is measured by the concentrated water quality measuring device 34, and water quality information of the first concentrated water is acquired (concentrated water quality measuring step).

本実施形態に係る凝集評価方法および凝集評価装置では、第1固液分離装置30および第2固液分離装置32で清澄側と濃縮側とに分離を行い、最終段の清澄側と第1段の濃縮側の両方の水質情報に基づいて凝集状態を評価する。これによって、凝集処理における凝集状態を適切に評価することができる。 In the flocculation evaluation method and flocculation evaluation apparatus according to the present embodiment, the first solid-liquid separator 30 and the second solid-liquid separator 32 perform separation into a clarifying side and a concentrating side, and the final stage clarifying side and the first stage Evaluate the flocculation state based on water quality information on both the concentration side. Thereby, the aggregation state in the aggregation process can be appropriately evaluated.

この水質測定結果に基づき、制御装置70により凝集処理装置5における凝集剤の注入率等の凝集条件が制御される(制御工程)。 Based on this water quality measurement result, the control device 70 controls the coagulation conditions such as the injection rate of the coagulant in the coagulation treatment device 5 (control step).

制御装置70は、例えば、プログラムを演算するCPU等の演算手段、プログラムや演算結果を記憶するROMおよびRAM等の記憶手段等を含んで構成されるマイクロコンピュータと電子回路等で構成される。制御装置70は、例えば、清澄水水質測定装置36、濃縮水水質測定装置34によって測定された清澄水の水質および濃縮水の水質の両方の水質情報に基づいて、凝集処理装置5における凝集処理の条件を制御する機能を有する。制御装置70は、例えば、清澄水水質測定装置36、濃縮水水質測定装置34によって測定された清澄水の水質および濃縮水の水質の両方の水質情報に基づいて、凝集処理装置5における凝集剤添加配管60に設置されたポンプの流量やバルブの開閉度等を調整して、被処理水への凝集剤の添加量を制御する機能を有する。 The control device 70 is composed of, for example, a microcomputer including a computing means such as a CPU that computes a program, a storage means such as a ROM and a RAM that stores the program and the results of the computation, and an electronic circuit. For example, the control device 70 controls the flocculation process in the flocculation treatment device 5 based on the water quality information of both the clear water quality and the concentrated water quality measured by the clear water quality measuring device 36 and the concentrated water quality measuring device 34. It has the ability to control conditions. For example, the control device 70 controls the addition of flocculant in the flocculant treatment device 5 based on the water quality information of both the clear water quality and the concentrated water quality measured by the clear water quality measuring device 36 and the concentrated water quality measuring device 34. It has a function of controlling the amount of flocculant added to the water to be treated by adjusting the flow rate of the pump installed in the piping 60, the opening/closing degree of the valve, etc.

本実施形態に係る凝集処理システムで用いられる凝集剤としては、無機凝集剤および高分子凝集剤のうちの少なくとも1つが用いられる。 As the flocculant used in the flocculation treatment system according to this embodiment, at least one of an inorganic flocculant and a polymer flocculant is used.

無機凝集剤としては、例えば、塩化第二鉄、ポリ硫酸第二鉄等の鉄系無機凝集剤、硫酸アルミニウム、ポリ塩化アルミニウム(PAC)等のアルミニウム系無機凝集剤等が挙げられる。 Examples of the inorganic flocculant include iron-based inorganic flocculants such as ferric chloride and polyferric sulfate, and aluminum-based inorganic flocculants such as aluminum sulfate and polyaluminum chloride (PAC).

無機凝集剤の添加量は、例えば、1~100mg/Lの範囲である。 The amount of the inorganic flocculant added is, for example, in the range of 1 to 100 mg/L.

高分子凝集剤としては、ノニオン性高分子凝集剤、アニオン性高分子凝集剤またはカチオン性高分子凝集剤等、特に制限されるものではないが、例えば、ポリアクリルアミド、ポリアクリル酸ナトリウム、アクリルアミド・アクリル酸塩共重合体、アクリルアミドプロパンスルフォン酸ナトリウム、キトサン、ジメチルアミノエチルメタクリレート、ジメチルアミノエチルアクリレートおよびポリアミジン等が挙げられる。高分子凝集剤は、1種単独でも、2種以上を組み合わせて用いてもよい。 Examples of polymer flocculants include nonionic polymer flocculants, anionic polymer flocculants, cationic polymer flocculants, etc., but examples include polyacrylamide, sodium polyacrylate, acrylamide, etc. Examples include acrylate copolymers, sodium acrylamide propane sulfonate, chitosan, dimethylaminoethyl methacrylate, dimethylaminoethyl acrylate, and polyamidine. The polymer flocculants may be used alone or in combination of two or more.

高分子凝集剤の添加量は、例えば、0.1~2mg/Lの範囲である。 The amount of the polymer flocculant added is, for example, in the range of 0.1 to 2 mg/L.

pH調整剤としては、塩酸、硫酸等の酸や、水酸化ナトリウム等のアルカリ剤である。pHは、例えば、4~11の範囲に調整すればよい。 Examples of pH adjusters include acids such as hydrochloric acid and sulfuric acid, and alkaline agents such as sodium hydroxide. The pH may be adjusted to a range of 4 to 11, for example.

凝集処理(凝集混和工程、フロック形成工程、分離工程)における液温度は、特に制限はなく、例えば、15~35℃の範囲である。粘性等によって分離性が変わるため、液温度はできるだけ一定になるように調整することが望ましい。 The liquid temperature in the flocculation treatment (coagulation mixing step, floc formation step, separation step) is not particularly limited, and is, for example, in the range of 15 to 35°C. Since separation properties vary depending on viscosity and other factors, it is desirable to adjust the liquid temperature to be as constant as possible.

凝集処理システムにおける処理対象である被処理水は、例えば、懸濁物質等を含む水であり、例えば、河川水、工業用水、排水等が挙げられる。 The water to be treated, which is the target of treatment in the coagulation treatment system, is, for example, water containing suspended substances, and includes, for example, river water, industrial water, wastewater, and the like.

以下、実施例および比較例を挙げ、本発明をより具体的に詳細に説明するが、本発明は、以下の実施例に限定されるものではない。 EXAMPLES Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples.

<実施例1>
図3の凝集評価装置を用いて、下記の条件で試験水の固液分離を行った。処理開始から80分~260分で純水を添加し、意図的に凝集を悪化させた。濁度の経時変化を図5に示す。
<Example 1>
Solid-liquid separation of the test water was performed using the flocculation evaluation apparatus shown in FIG. 3 under the following conditions. Pure water was added 80 minutes to 260 minutes after the start of treatment to intentionally worsen aggregation. Figure 5 shows the change in turbidity over time.

(実験条件)
試験水:濁度2度、凝集剤:ポリ塩化アルミニウム(PAC)40ppm、pH:4.0
第1固液分離装置、第2固液分離装置:曲がりチャネル
清澄水水質測定装置、濃縮水水質測定装置:濁度計(OPTEX製、TC-100)
(Experimental conditions)
Test water: turbidity 2 degrees, flocculant: polyaluminum chloride (PAC) 40 ppm, pH: 4.0
First solid-liquid separator, second solid-liquid separator: Bent channel Clear water quality measuring device, concentrated water quality measuring device: Turbidity meter (manufactured by OPTEX, TC-100)

<比較例1>
図1の凝集評価装置を用いて、実施例1と同じ試験水の固液分離を行った。比較例1では、清澄側の濁度を測定し、濃縮側の濁度は測定せずに処理を行った。濁度の経時変化を図6に示す。
<Comparative example 1>
Solid-liquid separation of the same test water as in Example 1 was performed using the flocculation evaluation apparatus shown in FIG. In Comparative Example 1, the turbidity on the clarification side was measured, and the treatment was performed without measuring the turbidity on the concentration side. Figure 6 shows the change in turbidity over time.

実施例1では、凝集が良好なときは、濃縮側と清澄側の濁度差が大きく、凝集が悪化したときに差が小さくなることが確認できる。 In Example 1, it can be confirmed that when the aggregation is good, the difference in turbidity between the concentrated side and the clarified side is large, and when the aggregation is deteriorated, the difference becomes small.

実施例1では、凝集の悪化を検知したとして、260分には水酸化ナトリウム水溶液を添加して試験水のpHを7.0±0.1に調整した。濁度の差が所定値を下回り、所定の時間が経過した後に、凝集条件の見直しを行った(今回の実験では水酸化ナトリウム水溶液を添加してpHの最適化を実施した)結果、濁度の差が再び大きくなった。 In Example 1, the pH of the test water was adjusted to 7.0±0.1 by adding an aqueous sodium hydroxide solution at 260 minutes, assuming that deterioration of aggregation was detected. After the difference in turbidity fell below a predetermined value and a predetermined time had elapsed, the flocculation conditions were reviewed (in this experiment, an aqueous sodium hydroxide solution was added to optimize the pH). The difference has increased again.

比較例1の清澄側の濁度の結果を見ると、凝集の良否によらず濁度に変化が見られないことがわかる。変化がなければ、凝集処理装置の制御に利用することができない。 Looking at the results of the turbidity on the clarified side of Comparative Example 1, it can be seen that there is no change in the turbidity regardless of the quality of aggregation. If there is no change, it cannot be used to control the aggregation treatment device.

各時間における凝集沈殿の処理水濁度を表1に示す。 Table 1 shows the turbidity of the treated water due to coagulation and precipitation at each time.

Figure 2023183764000002
Figure 2023183764000002

実施例1では凝集悪化を検知して、凝集状態を回復することができ、沈殿処理水濁度の上昇は一時的であり、その後、回復した。比較例1では凝集悪化を検知することができないため、沈殿処理水濁度が上昇し続けた。 In Example 1, it was possible to detect the deterioration of aggregation and recover the agglomeration state, and the increase in turbidity of the sedimentation treated water was temporary, and then it recovered. In Comparative Example 1, the turbidity of the precipitated water continued to rise because deterioration of aggregation could not be detected.

このように、実施例の方法によって、凝集処理における凝集状態を適切に評価することができた。 In this manner, the agglomeration state in the aggregation treatment could be appropriately evaluated by the method of the example.

1,3 凝集評価装置、5 凝集処理装置、7 凝集処理システム、10 固液分離装置、12,36 清澄水水質測定装置、14,34 濃縮水水質測定装置、16,38 被評価水配管、18 清澄水配管、20 濃縮水配管、30 第1固液分離装置、32 第2固液分離装置、40 第1清澄水配管、42 第1濃縮水配管、44 第2清澄水配管、46 第2濃縮水配管、50 凝集混和槽、52 分離装置、54 被処理水配管、56 凝集液配管、58 処理水配管、60 凝集剤添加配管、70 制御装置。 1, 3 Coagulation evaluation device, 5 Coagulation treatment device, 7 Coagulation treatment system, 10 Solid-liquid separation device, 12, 36 Clear water quality measurement device, 14, 34 Concentrated water quality measurement device, 16, 38 Water piping to be evaluated, 18 Clear water piping, 20 Concentrated water piping, 30 First solid-liquid separator, 32 Second solid-liquid separator, 40 First clear water piping, 42 First concentrated water piping, 44 Second clear water piping, 46 Second concentration Water piping, 50 coagulation mixing tank, 52 separation device, 54 treated water piping, 56 flocculating liquid piping, 58 treated water piping, 60 flocculant addition piping, 70 control device.

Claims (10)

凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離装置の前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価することを特徴とする凝集評価方法。 The flocculation process is performed based on the water quality information of both the clear water quality and the concentrated water quality of the solid-liquid separator that separates the evaluated water containing flocculated flocs obtained by the flocculation treatment into clear water and concentrated water. A flocculation evaluation method characterized by evaluating the flocculation state during processing. 請求項1に記載の凝集評価方法であって、
前記水質情報が、前記濃縮水の濁度と前記清澄水の濁度との濁度差であることを特徴とする凝集評価方法。
The agglomeration evaluation method according to claim 1,
A flocculation evaluation method characterized in that the water quality information is a turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water.
請求項2に記載の凝集評価方法であって、
前記濁度差が小さくなったときに凝集悪化と判断し、前記濁度差が大きくなったときに凝集良好と判断することを特徴とする凝集評価方法。
The agglomeration evaluation method according to claim 2,
A flocculation evaluation method characterized in that when the turbidity difference becomes small, it is determined that aggregation is deteriorated, and when the turbidity difference becomes large, it is determined that aggregation is good.
凝集処理で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段と、
前記清澄水の水質を測定する清澄水水質測定手段と、
前記濃縮水の水質を測定する濃縮水水質測定手段と、
を備え、
前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価することを特徴とする凝集評価装置。
solid-liquid separation means for separating evaluated water containing flocculated flocs obtained in the flocculation treatment into clear water and concentrated water;
Clear water quality measuring means for measuring the quality of the clear water;
Concentrated water quality measuring means for measuring the water quality of the concentrated water;
Equipped with
A flocculation evaluation device characterized in that the flocculation state in the flocculation process is evaluated based on water quality information of both the water quality of the clear water and the water quality of the concentrated water.
請求項4に記載の凝集評価装置であって、
前記水質情報が、前記濃縮水の濁度と前記清澄水の濁度との濁度差であることを特徴とする凝集評価装置。
The agglomeration evaluation device according to claim 4,
A flocculation evaluation device, wherein the water quality information is a turbidity difference between the turbidity of the concentrated water and the turbidity of the clear water.
請求項5に記載の凝集評価装置であって、
前記濁度差が小さくなったときに凝集悪化と判断し、前記濁度差が大きくなったときに凝集良好と判断することを特徴とする凝集評価装置。
The agglomeration evaluation device according to claim 5,
An agglomeration evaluation device characterized in that when the turbidity difference becomes small, it is determined that the aggregation is deteriorated, and when the turbidity difference becomes large, it is determined that the aggregation is good.
被処理水に凝集剤を添加して凝集処理を行う凝集処理工程を含み、
前記凝集処理工程で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離装置の前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価することを特徴とする凝集処理方法。
Including a flocculation treatment process in which a flocculant is added to the water to be treated to perform flocculation treatment,
Based on the water quality information of both the water quality of the clear water and the water quality of the concentrated water of a solid-liquid separator that separates the evaluated water containing the flocculated flocs obtained in the coagulation treatment step into clear water and concentrated water. An aggregation treatment method characterized by evaluating the aggregation state in the aggregation treatment.
請求項7に記載の凝集処理方法であって、
前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理工程における凝集処理の条件を制御することを特徴とする凝集処理方法。
The aggregation treatment method according to claim 7,
A flocculation treatment method, characterized in that conditions for flocculation treatment in the flocculation treatment step are controlled based on water quality information of both the water quality of the clear water and the water quality of the concentrated water.
被処理水に凝集剤を添加して凝集処理を行う凝集処理装置と、
前記凝集処理装置で得られた凝集フロックを含む被評価水について清澄水と濃縮水とに分離を行う固液分離手段と、
前記清澄水の水質を測定する清澄水水質測定手段と、
前記濃縮水の水質を測定する濃縮水水質測定手段と、
を備え、
前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理における凝集状態を評価することを特徴とする凝集処理システム。
A flocculation treatment device that performs flocculation treatment by adding a flocculant to water to be treated;
solid-liquid separation means for separating the water to be evaluated containing the flocculated flocs obtained by the flocculation treatment device into clear water and concentrated water;
Clear water quality measuring means for measuring the quality of the clear water;
Concentrated water quality measuring means for measuring the water quality of the concentrated water;
Equipped with
A flocculation treatment system, characterized in that the flocculation state in the flocculation treatment is evaluated based on water quality information of both the water quality of the clear water and the water quality of the concentrated water.
請求項9に記載の凝集処理システムであって、
前記清澄水の水質および前記濃縮水の水質の両方の水質情報に基づいて前記凝集処理装置における凝集処理の条件を制御する制御手段をさらに備えることを特徴とする凝集処理システム。
The aggregation treatment system according to claim 9,
A flocculation treatment system further comprising a control means for controlling conditions for flocculation treatment in the flocculation treatment apparatus based on water quality information of both the water quality of the clear water and the water quality of the concentrated water.
JP2022097450A 2022-06-16 2022-06-16 Flocculation evaluation method, flocculation evaluation device, flocculation treatment method, and flocculation treatment system Pending JP2023183764A (en)

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